Claims Analysis
Total Claims: 14
Claim 1
Independent Claim
147 words
A process for the deinking of waste newsprint, which comprises steps for (a) converting the waste newsprint to a pulp, (b) contacting and agitating the pulp in an aqueous medium containing a deinking agent comprising a mixture of (i) a water-soluble C 9 to C 16 alkanol ethoxylate component having an average of about 6.5 to 20 oxyethylene units per ethoxylate molecule and (ii) an oil-soluble C 9 to C 16 alkanol ethoxylate component having an average of about 0.5 to 3.5 oxyethylene units per ethoxylate molecule, said mixture containing the respective components (i) and (ii) in a relative weight ratio in the range from about 2:1 to 1:3, and said mixture being present in said aqueous medium in an amount between about 0.1 and 5 percent by weight based on the dry weight of the newsprint fiber, and (c) recovering deinked pulp from the aqueous medium.
Claim 2
Dependent Claim
147 words
A process for the deinking of waste newsprint, which comprises steps for (a) converting the waste newsprint to a pulp, (b) contacting and agitating the pulp in an aqueous medium containing a deinking agent comprising a mixture of (i) a water-soluble C 9 to C 16 alkanol ethoxylate component having an average of about 6.5 to 20 oxyethylene units per ethoxylate molecule and (ii) an oil-soluble C 9 to C 16 alkanol ethoxylate component having an average of about 0.5 to 3.5 oxyethylene units per ethoxylate molecule, said mixture containing the respective components (i) and (ii) in a relative weight ratio in the range from about 2:1 to 1:3, and said mixture being present in said aqueous medium in an amount between about 0.1 and 5 percent by weight based on the dry weight of the newsprint fiber, and (c) recovering deinked pulp from the aqueous medium.
Claim 3
Dependent Claim
24 words
The process of claim 1, wherein the respective weight ratio of components (i) and (ii) is in the range from about 1.85:1 to 1:2.
Claim 4
Dependent Claim
23 words
The process of claim 2, wherein the water-soluble alkanol ethoxylate has an average of about 7 to 15 oxyethylene units per ethoxylate molecule.
Claim 5
Dependent Claim
23 words
The process of claim 3, wherein the oil-soluble alkanol ethoxylate has an average of about 1 to 3 oxyethylene units per ethoxylate molecule.
Claim 6
Dependent Claim
24 words
The process of claim 4, wherein the respective weight ratio of components (i) and (ii) is in the range from about 1.6:1 to 1:1.
Claim 7
Dependent Claim
23 words
The process of claim 5, wherein the water-soluble alkanol ethoxylate has an average of about 8 to 13 oxyethylene units per ethoxylate molecule.
Claim 8
Dependent Claim
23 words
The process of claim 6, wherein the oil-soluble alkanol ethoxylate has an average of about 1.5 to 3 oxyethylene units per ethoxylate molecule.
Claim 9
Dependent Claim
21 words
The process of claim 7, wherein the water-soluble and the oil-soluble ethoxylates are ethoxylates of C 11 to C 15 alkanols.
Claim 10
Dependent Claim
35 words
The process of claim 1, wherein the aqueous medium contains between about 1 and 5%w of pulp and step (b) of the process is carried out at a temperature between about 70° and 130° F.
Claim 11
Dependent Claim
34 words
The process of claim 4, wherein the aqueous medium contains between about 1 and 5%w pulp and step (b) of the process is carried out at a temperature between about 70° and 130° F.
Claim 12
Dependent Claim
34 words
The process of claim 7, wherein the aqueous medium contains between about 1 and 5%w pulp and step (b) of the process is carried out at a temperature between about 70° and 130° F.
Claim 13
Dependent Claim
34 words
The process of claim 8, wherein the aqueous medium contains between about 1 and 5%w pulp and step (b) of the process is carried out at a temperature between about 70° and 130° F.
Claim 14
Dependent Claim
23 words
The process of claim 12, wherein the water-soluble and oil-soluble ethoxylates have both been derived from alkanols which are predominantly linear and primary.